US4218304A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Retorting hydrocarbonaceous solids
Assignee: Atlantic Richfield Co
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Filing: 1978-12-28
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Granted: 1980-08-19
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Expires: 1998-12-28
Abstract
Abstract Mined, crushed hydrocarbonaceous solids are pyrolyzed in a retort with a gas containing hydrocarbons. The gas is heated to a suitable temperature of at least 600° F. Thereafter, a relatively small amount of oxygen is added to the heated gas outside the retort. The resulting mixture is then flowed into the retort. The amount of oxygen is theoretically sufficient to raise the temperature of the heated gas at least 100° F., but is less than the amount theoretically sufficient to react with all of the hydrocarbons in the heated gas. The process is applicable to any type of retort wherein a retort recycle gas containing hydrocarbons is heated outside the retort and is then injected into the retort to provide a source of heat for pyrolyzing hydrocarbonaceous solids in the retort. The advantages of this modified indirect heated retorting method depends on the type of retort. This method provides added control over carbonate decomposition, coking or carbonization of the gas during heating, total gas flow, process variations, and the heat requirements and thermal efficiency of the process.
Inventors
- 👤 Ralph E. Styring, Jr.
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 01:01
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/02; C10B; C10B49/00; C10B49/02
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
255 words
A method of retorting of the hydrocarbonaceous matter in crushed mined hydrocarbonaceous solids comprising: (a) feeding crushed mined hydrocarbon solids to a retort; (b) heating at least one moving stream of a first gas to a temperature of at least 600° F., said first gas being at least partially comprised of gaseous hydrocarbons derived from retorting hydrocarbonaceous solids; (c) mixing outside of said retort at least a portion of said first gas heated in step (b) with a second gas, said second gas being at least partially comprised of molecular oxygen and being at a temperature less than the temperature of said portion of said heated first gas, said second gas being in an amount which is less than the amount needed to supply enough oxygen to react with all of the hydrocarbons in said portion of said heated first gas and which is at least as great as the calculated amount needed to supply enough oxygen to raise the temperature of said portion of said heated first gas at least 100° F. when, for purposes of such calculation, it is assumed that all of the oxygen in said second gas reacts with hydrocarbons in said portion of said heated first gas; (d) flowing at least a portion of the mixture produced in step (c) into said retort at at least one point; and (e) operating said retort at a temperature of at least 700° F. to convert a substantial portion of the hydrocarbonaceous matter in the retorted hydrocarbonaceous solids to gases and oil vapors.
Claim 2
Independent Claim
255 words
A method of retorting of the hydrocarbonaceous matter in crushed mined hydrocarbonaceous solids comprising: (a) feeding crushed mined hydrocarbon solids to a retort; (b) heating at least one moving stream of a first gas to a temperature of at least 600° F., said first gas being at least partially comprised of gaseous hydrocarbons derived from retorting hydrocarbonaceous solids; (c) mixing outside of said retort at least a portion of said first gas heated in step (b) with a second gas, said second gas being at least partially comprised of molecular oxygen and being at a temperature less than the temperature of said portion of said heated first gas, said second gas being in an amount which is less than the amount needed to supply enough oxygen to react with all of the hydrocarbons in said portion of said heated first gas and which is at least as great as the calculated amount needed to supply enough oxygen to raise the temperature of said portion of said heated first gas at least 100° F. when, for purposes of such calculation, it is assumed that all of the oxygen in said second gas reacts with hydrocarbons in said portion of said heated first gas; (d) flowing at least a portion of the mixture produced in step (c) into said retort at at least one point; and (e) operating said retort at a temperature of at least 700° F. to convert a substantial portion of the hydrocarbonaceous matter in the retorted hydrocarbonaceous solids to gases and oil vapors.
Claim 3
Dependent Claim
22 words
The method of claim 1 wherein in step (b), the first gas is heated to a temperature of at least 900° F.
Claim 4
Dependent Claim
21 words
The method of claim 1 wherein in step (d), the mixture is flowed into said retort at at least two points.
Claim 5
Dependent Claim
22 words
The method of claim 3 wherein in step (b), the first gas is heated to a temperature of at least 900° F.
Claim 6
Dependent Claim
37 words
The method of claim 1 wherein in step (c), the amount of said second gas is calculated to raise the temperature of said heated first gas mixed with said second gas between 100° F. and 900° F.
Claim 7
Dependent Claim
22 words
The method of claim 5 wherein in step (b), the first gas is heated to a temperature of at least 900° F.
Claim 8
Dependent Claim
21 words
The method of claim 5 wherein in step (d), the mixture is flowed into said retort at at least two points.
Claim 9
Dependent Claim
22 words
The method of claim 7 wherein in step (b), the first gas is heated to a temperature of at least 900° F.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1983-08-19 | 1984-02-18 | 1984-08-19 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1987-08-19 | 1988-02-18 | 1988-08-19 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1991-08-19 | 1992-02-18 | 1992-08-19 | $7700.00 | Window Closed / Lapsed |